Method to produce and recover levulinic acid and/or gamma-valerolactone from aqueous solutions using alkylphenols

a technology of gamma-valerolactone and aqueous solution, which is applied in the preparation of carboxylic compounds, organic chemistry, chemistry apparatus and processes, etc., can solve the problems of difficult and economically unfeasible separation and purification steps, complicated fuels and chemicals from biomass, etc., and achieve easy and cost-efficient recovery, simple distillation, and enhanced gvl concentration

Active Publication Date: 2012-11-29
WISCONSIN ALUMNI RES FOUND
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  • Abstract
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  • Claims
  • Application Information

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Benefits of technology

[0010]Another advantage of this strategy is that the lower degrees of functionality and boiling points of these platform molecules allow for catalytic processing in the vapor phase and/or in organic solvents. This alleviates the need to develop heterogeneous catalysts that are stable under more demanding hydro-thermal reaction conditions. One such platform molecule is levulinic acid (LA) (3, 4) from which a variety of fuels and chemicals can be made, such as valeric acid esters (5), methyltetrahydrofuran (6-8), and esters and ketals of LA (9). Another building block from the reduction of LA is γ-valerolactone (GVL) (10, 11), which can be used directly as a fuel additive (12), or as a precursor for fuels (13) and chemicals (14, 15). While LA can be formed in significant yields (>50%) by cellulose deconstruction in aqueous solutions of mineral acids such as sulfuric acid (SA) (16, 17), a challenge for profitable, large-scale production of LA and its derivatives has been separating the LA from the mineral acid used in the process. This is necessary so that the LA can be further processed downstream without the negative effects of the mineral acid (18).
[0011]In the present method, alkylphenol (AP) solvents (19) are used as a partitioning agent in a method to produce LA and/or GVL from biomass in general, and lignocellulosic biomass in particular. As illustrated schematically in FIG. 1, AP solvents can be used to selectively extract LA from aqueous solutions after a cellulose deconstruction step. In addition, AP solvents extract GVL from water with a higher partition coefficient (the concentration of the solute in the organic phase divided by the concentration of the solute in the aqueous phase) compared to LA. Accordingly, the GVL concentration in the AP solvent can be increased by the conversion of LA to GVL, combined with the recycle of this stream for successive extractions. Importantly, a preferred carbon-supported RuSn catalyst (20, 21) can be used to selectively reduce LA to GVL by hydrogenation in the presence of AP, without hydrogenation of the solvent. This is a critical discovery in that ...

Problems solved by technology

Making fuels and chemicals from biomass is complicated by the need to separate and to purify the intermediate platform molecules at high yields.
Conv...

Method used

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  • Method to produce and recover levulinic acid and/or gamma-valerolactone from aqueous solutions using alkylphenols
  • Method to produce and recover levulinic acid and/or gamma-valerolactone from aqueous solutions using alkylphenols
  • Method to produce and recover levulinic acid and/or gamma-valerolactone from aqueous solutions using alkylphenols

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[0064]The following Examples are included solely to provide a more complete disclosure of the method described and claimed herein. The Examples do not limit the scope of the claims in any fashion.

1. Materials and Methods

1.1. Liquid-Liquid Extractions

[0065]1.1.1. Simulated Feed

[0066]Liquid-liquid extractions were carried out in 20 mL glass vials. Typically, 4 g of aqueous solution with 0.5 M sulfuric acid (Sigma-Aldrich, St. Louis, Mo., USA, >96%), LA (Sigma-Aldrich, St. Louis, Missouri, USA 98%), FA (Sigma-Aldrich, 98-100%) and / or GVL (Sigma-Aldrich, >98%), in the concentrations indicated, plus 4 g of the indicated AP (2-sec-butylphenol (Alfa Aesar, Ward Hill, Mass., USA >98%) 4-n-pentylphenol (Sigma-Aldrich, >98%), 4-n-hexylphenol (Acros Organics, Geel, Belgium, 98%) and GVL, when used, were added to the vial and shaken vigorously for one minute. After the two phases separated, the organic top phase contained SBP, GVL, LA and FA, and the aqueous bottom phase contained water, sulfur...

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Abstract

A method to produce levulinic acid (LA) and γ-valerolactone (GVL) from biomass-derived cellulose by selective extraction of LA by alkylphenol (AP) and hydrogenation of LA, in which mineral acid used in the method is recycled and the final concentration of GVL is increased by successive extraction/hydrogenation steps to allow for effective separation by distillation.

Description

FEDERAL FUNDING STATEMENT[0001]This invention was made with government support under W911NF-09-0010 awarded by the ARMY / ARO. The government has certain rights in the invention.BACKGROUND[0002]Significant advances have been made in recent years with respect to using heterogeneous catalysts for converting biomass-derived compounds to fuels and chemicals. Conventional approaches deconstruct solid cellulose into smaller molecules that are soluble in various solvents (e.g., water, ionic liquids), thereby allowing transport of these reactants to the active sites on the heterogeneous catalyst, the majority of which are located within the pores of a high-surface area material. A difficulty in implementing this strategy is that chemical components used to deconstruct solid cellulose (e.g., sulfuric acid) may alter the performance of heterogeneous catalysts used subsequently to convert the soluble biomass-derived reactants to the desired fuels and / or chemicals. As a result, costly purificatio...

Claims

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Application Information

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IPC IPC(8): C07D307/33C07C59/185
CPCC07C51/48C07C67/04C07C67/08C07D307/33C07C69/716C07C59/185
Inventor DUMESIC, JAMESBOND, JESSEALONSO, DAVIDROOT, THATCHER
Owner WISCONSIN ALUMNI RES FOUND
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